公开(公告)号：US12129216B2

公开(公告)日：2024-10-29

申请号：US17906234

申请日：2021-03-12

申请人： CHINA PETROLEUM & CHEMICAL CORPORATION ,  SHANGHAI RESEARCH INSTITUTE OF PETROCHEMICAL TECHNOLOGY, SINOPEC

发明人： Guozhen Qi ,  Jing Cao ,  Xiaohong Li ,  Hongtao Wang ,  Li Wang ,  Yanxue Wang

IPC分类号： C07C1/20 ,  B01J8/24 ,  B01J29/85 ,  C07C11/06

CPC分类号： C07C1/20 ,  B01J8/24 ,  B01J29/85 ,  C07C11/06

摘要： The invention relates to a process of converting methanol in a fluidized bed reactor comprising feeding a methanol-containing feedstock into a fluidized bed reactor, contacting the feedstock with a catalyst, to produce a product comprising ethylene and propylene under effective conditions; the fluidized bed reactor comprises a diluent-phase zone and a dense-phase zone, wherein the diluent-phase temperature difference between any regions of the diluent-phase zone having a methanol concentration of more than 0.1 wt % (preferably more than 0.01 wt %) in the fluidized bed reactor is controlled to be less than 20° C., and the dense-phase temperature difference between any regions in the dense-phase zone having a methanol concentration of more than 0.1 wt % (preferably more than 0.01 wt %) in the fluidized bed reactor is controlled to be less than 10° C.

公开(公告)号：US12116331B2

公开(公告)日：2024-10-15

申请号：US17286576

申请日：2019-10-17

申请人： CHINA PETROLEUM & CHEMICAL CORPORATION ,  SHANGHAI RESEARCH INSTITUTE OF PETROCHEMICAL TECHNOLOGY SINOPEC

发明人： Siqing Zhong ,  Jun Xu ,  Le Zhao ,  Lianghua Wu

IPC分类号： B01J8/18 ,  B01J8/00 ,  B01J8/24 ,  B01J21/08 ,  B01J23/72 ,  B01J23/94 ,  B01J35/40 ,  B01J38/06 ,  C07C209/36

CPC分类号： C07C209/36 ,  B01J8/0055 ,  B01J8/1809 ,  B01J8/1827 ,  B01J8/24 ,  B01J21/08 ,  B01J23/72 ,  B01J23/94 ,  B01J35/40 ,  B01J38/06 ,  B01J2208/00752

摘要： A gas replacement process and a gas replacement apparatus are employed, in the nitro compound hydrogenation reaction process. The gas replacement process at least includes a first step of subjecting a stream to be replaced to the gas replacement in presence of a first replacement gas, and then a second step of subjecting to the gas replacement in presence of the second replacement gas. Assuming the superficial velocity of the first replacement gas is V1, and the superficial velocity of the second replacement gas is V2, then V2/V1≥1.5.

公开(公告)号：US20240262771A1

公开(公告)日：2024-08-08

申请号：US18562876

申请日：2022-05-20

申请人： CHINA PETROLEUM & CHEMICAL CORPORATION ,  SHANGHAI RESEARCH INSTITUTE OF PETROCHEMICAL TECHNOLOGY, SINOPEC

发明人： Weimin YANG ,  Xiangcheng LI ,  Zhendong WANG ,  Xiao HAN ,  Xinqiang FENG ,  Zhiqing YUAN ,  Jian QIAO ,  Chuang LIU ,  Dawei LAN

IPC分类号： C07C29/17

CPC分类号： C07C29/17 ,  C07C2521/18

摘要： A biphasic solvent system for converting biomass to prepare 2,5-hexanedione and a one-pot process for catalytically converting biomass to prepare 2,5-hexanedione with said biphasic solvent system are provided. The process includes the steps of contacting and reacting a biomass raw material with a hydrogenation catalyst using hydrogen gas as a hydrogen source in a heterogeneous system formed from an organic solvent, an inorganic salt and water to obtain 2,5-hexanedione. The hydrogenation catalyst includes a hydrogenation active component and a support. The support is selected from one or more of hydrophobic active carbon and graphene. The process can achieve efficient conversion of biomass without the participation of acid catalysts, and have a very high selectivity for the product 2,5-hexanedione.

公开(公告)号：US20240246052A1

公开(公告)日：2024-07-25

申请号：US18566128

申请日：2022-06-23

申请人： CHINA PETROLEUM & CHEMICAL CORPORATION ,  SHANGHAI RESEARCH INSTITUTE OF PETROCHEMICAL TECHNOLOGY, SINOPEC

发明人： Hongyuan ZONG ,  Guozhen QI ,  Pan GAO ,  Xiaohong LI ,  Jing CAO ,  Zhinan YU ,  Yanxue WANG ,  Fei PENG

IPC分类号： B01J8/18 ,  B01J8/00 ,  B01J8/26 ,  C07C1/24

CPC分类号： B01J8/1827 ,  B01J8/0055 ,  B01J8/1863 ,  B01J8/26 ,  C07C1/24 ,  B01J2208/00752 ,  B01J2208/00849 ,  B01J2208/00902 ,  B01J2208/00938 ,  C07C2529/40

摘要： A fluidized bed reactor, a device for preparing low-carbon olefin, and a method for preparing low-carbon olefin are provided. The reaction zone of the fluidized bed reactor is sequentially, from bottom to top, provided with a raw material first distributor, a raw material second distributor and a catalyst distributor; the catalyst distributor is connected with the catalyst second feeding inlet; a dense-phase zone is formed between the raw material first distributor and the raw material second distributor, and the area where the catalyst distributor is located is formed as a catalyst distribution zone connected with the dense-phase zone; and at least one catalyst first feeding inlet(s) is provided on the side wall of reactor of the dense-phase zone. The distribution of the catalyst and the full contact of the catalyst with the raw materials can be achieved using the fluidized bed reactor and the device.

公开(公告)号：US20240239689A1

公开(公告)日：2024-07-18

申请号：US18562069

申请日：2022-05-16

申请人： CHINA PETROLEUM & CHEMICAL CORPORATION ,  SHANGHAI RESEARCH INSTITUTE OF PETROCHEMICAL TECHNOLOGY, SINOPEC

发明人： Tongbao ZHANG ,  Yu ZHANG ,  Biwei WANG ,  Ye ZHU ,  Fang CHEN ,  Huanxin GAO

IPC分类号： C01G53/00 ,  H01M4/02 ,  H01M4/505 ,  H01M4/525 ,  H01M10/052

CPC分类号： C01G53/50 ,  H01M4/505 ,  H01M4/525 ,  H01M10/052 ,  C01P2002/72 ,  C01P2004/03 ,  C01P2004/32 ,  C01P2004/50 ,  C01P2004/51 ,  C01P2004/61 ,  C01P2004/84 ,  C01P2006/40 ,  H01M2004/028

摘要： A lithium battery positive electrode material precursor and its preparation method and application are provided. The positive electrode material precursor has the chemical formula NixCoyMzTp(OH)q and contains secondary particles in the form of microspheres formed by agglomeration of primary particles. The microspheres have a three-layer structure from the inside to the outside, namely an inner core layer, a middle layer and an outermost layer. The ratio of the intensity of the (110) and (102) crystal planes diffraction peaks expressed as peak height in the XRD diffraction pattern of the inner core layer of the microsphere is 1.0-8.0. The positive electrode material prepared by using the positive electrode material precursor has high discharge specific capacity and good cycle stability and can be used in high-performance lithium batteries.

公开(公告)号：US20230405563A1

公开(公告)日：2023-12-21

申请号：US18249718

申请日：2021-10-19

申请人： CHINA PETROLEUM & CHEMICAL CORPORATION ,  SHANGHAI RESEARCH INSTITUTE OF PETROCHEMICAL TECHNOLOGY, SINOPEC

发明人： Chang LIU ,  Yangdong WANG ,  Zaiku XIE ,  Su LIU ,  Haibo ZHOU ,  Junjie SU ,  Wenqian JIAO ,  Lin ZHANG

IPC分类号： B01J29/48 ,  B01J35/02 ,  B01J37/08 ,  B01J23/34 ,  B01J23/26 ,  C01B39/40 ,  C01B39/36 ,  C01B39/02 ,  C07C1/04

CPC分类号： B01J29/48 ,  B01J35/023 ,  B01J37/082 ,  B01J23/34 ,  B01J23/26 ,  C01B39/40 ,  C01B39/365 ,  C01B39/026 ,  C07C1/043 ,  C07C1/0445 ,  C01P2002/72 ,  C01P2004/03 ,  B01J2229/186 ,  C07C2529/40

摘要： A catalyst contains a metal oxide, and a molecular sieve, in a crystal form, having a topological pore structure. The metal oxide is centrally distributed on the surface of the molecular sieve. Grains of the molecular sieve are exposed to at least three families of crystal planes. The family of crystal plane with the largest pore size in topology is occupied by the metal oxide by no more than 30%, preferably no more than 20%, or no more than 10%.

公开(公告)号：US11571673B2

公开(公告)日：2023-02-07

申请号：US16763917

申请日：2018-11-09

申请人： CHINA PETROLEUM & CHEMICAL CORPORATION ,  SHANGHAI RESEARCH INSTITUTE OF PETROCHEMICAL TECHNOLOGY SINOPEC

发明人： Le Zhao ,  Lianghua Wu

IPC分类号： B01J8/44 ,  B01J8/18 ,  C07C253/26

摘要： A fluid distributor includes one or more fluid transport main pipe. The fluid transport main pipe is configured to assume a closed shape when its centerlines and/or centerline extensions are joined end-to-end. Each of the fluid transport main pipe has at least one fluid inlet and is connected with a plurality of fluid transport branch pipes. Each of the fluid transport branch pipes has a plurality of open pores disposed along the length of the fluid transport branch pipe and a connection portion. The connection portion is configured to connect the fluid transport branch pipe to the housing after the fluid transport branch pipe passes through the housing of the vessel into the inner cavity.

公开(公告)号：US20220250927A1

公开(公告)日：2022-08-11

申请号：US17626077

申请日：2020-07-09

申请人： CHINA PETROLEUM & CHEMICAL CORPORATION ,  SHANGHAI RESEARCH INSTITUTE OF PETROCHEMICAL TECHNOLOGY, SINOPEC

发明人： Weimin YANG ,  Wenhua FU ,  Zhiqing YUAN ,  Zhendong WANG ,  Jiawei TENG ,  Weichuan TAO ,  Shengli ZHAO

IPC分类号： C01B39/48 ,  B01J20/18

摘要： A silicon- and germanium-based molecular sieve has a framework chemical composition as represented by the formula “SiO2.1/nGeO2”. The silicon/germanium molar ratio is 0.1n30. The molecular sieve has a unique X-ray diffraction pattern. It can be used in adsorptive separation, ion exchange, and catalytic conversion of organic compounds.

公开(公告)号：US11193055B2

公开(公告)日：2021-12-07

申请号：US16691289

申请日：2019-11-21

申请人： CHINA PETROLEUM & CHEMICAL CORPORATION ,  SHANGHAI RESEARCH INSTITUTE OF PETROCHEMICAL TECHNOLOGY, SINOPEC

发明人： Yingcheng Li ,  Songyuan Gu ,  Weidong Zhang ,  Xinning Bao ,  Ou Sha ,  Zhiqin Shen ,  Yiqing Yang ,  Xiaodong Zhai

IPC分类号： C09K8/584

摘要： This invention relates to a surfactant composition, production and use thereof in tertiary oil recovery. The present surfactant composition comprises a cationic-nonionic surfactant and an anionic surfactant, and exhibits significantly improved interfacial activity and stability as compared with the prior art. With the present surfactant composition, a flooding fluid composition for tertiary oil recovery with improved oil displacement efficiency and oil washing capability as compared with the prior art could be produced.

公开(公告)号：US20210371370A1

公开(公告)日：2021-12-02

申请号：US17286666

申请日：2019-10-17

申请人： CHINA PETROLEUM & CHEMICAL CORPORATION ,  SHANGHAI RESEARCH INSTITUTE OF PETROCHEMICAL TECHNOLOGY SINOPEC

发明人： Siqing ZHONG ,  Jun XU ,  Le ZHAO ,  Lianghua WU

IPC分类号： C07C209/36 ,  B01J8/24 ,  B01J8/18 ,  B01J8/00 ,  B01J21/08 ,  B01J23/72 ,  B01J35/02 ,  B01J23/94 ,  B01J38/06

摘要： The present invention relates to a nitro compound hydrogenation reaction process and hydrogenation reaction apparatus, which can achieve the objects of the continuous reaction of the nitro compound and the long-period run of regeneration and activation. The nitro compound hydrogenation reaction process comprises a hydrogenation step, a regeneration step, an optional activation step and a recycling step. There exists at least one step of degassing the spent catalyst between the hydrogenation step and the regeneration step. According to circumstances, there exists at least one step of degassing the regenerated catalyst between the regeneration step and the activation step.